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1.发明申请Use of Solvent Stream as Motive Fluid in Ejector Unit for Regenerating Solvent for Absorption Unit 审中-公开使用溶剂流作为吸附剂再生溶剂的喷射器中的动力流体公开(公告)号：US20090241778A1
公开(公告)日：2009-10-01
申请号：US12055909
申请日：2008-03-26
CPC分类号： B01D53/1425 , B01D53/1475 , B01D2257/504 , Y02A50/2342 , Y02C10/04 , Y02C10/06
摘要： The invention provides a process and system for regenerating a solvent used to remove carbon dioxide from feed gases, such as natural gas and synthesis gas. The process and system employs an eductor or ejector as an alternative to the prior art's vacuum compressor that is placed on the vapor stream from a vapor flash. This process and system saves substantial capital and operating costs over the prior art.
摘要翻译： 本发明提供了用于再生用于从诸如天然气和合成气的原料气中除去二氧化碳的溶剂的方法和系统。 该方法和系统采用喷射器或喷射器作为现有技术的真空压缩机的替代物，其被放置在来自蒸气闪蒸的蒸气流中。 与现有技术相比，该过程和系统节省了大量资本和运营成本。
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公开(公告)号：US07687048B1
公开(公告)日：2010-03-30
申请号：US11540088
申请日：2006-09-28
CPC分类号： C07C7/12 , B01D53/1425 , B01D53/1475 , Y02C10/06 , Y02P20/152 , Y02P30/464
摘要： Processing schemes and arrangements for the amine treatment of high olefin content (e.g., ethylene-rich) carbon dioxide-containing streams such as for the effective separation and removal of carbon dioxide therefrom are provided. Corresponding or associated processing schemes and arrangements for the catalytic cracking of a heavy hydrocarbon feedstock and obtaining light olefins substantially free of carbon dioxide via absorption-based product recovery are also provided.
摘要翻译： 提供了用于胺处理高烯烃含量（例如富含乙烯的二氧化碳）流的方法和装置，以便有效分离和除去二氧化碳。 还提供了通过基于吸收的产物回收的重烃原料的催化裂化和获得基本上不含二氧化碳的轻质烯烃的相应或相关的处理方案和装置。
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3.发明授权公开(公告)号：US07973209B1
公开(公告)日：2011-07-05
申请号：US11541310
申请日：2006-09-28
摘要： Processing schemes and arrangements for the catalytic cracking of a heavy hydrocarbon feedstock and obtaining light olefins substantially free of carbon dioxide via amine treatment and employing fractionation processing are provided.
摘要翻译： 提供了重烃原料的催化裂化和通过胺处理和采用分馏处理获得基本上不含二氧化碳的轻质烯烃的加工方案和装置。
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4.发明申请公开(公告)号：US20080081938A1
公开(公告)日：2008-04-03
申请号：US11541200
申请日：2006-09-28
IPC分类号： C07C4/02
CPC分类号： C07C7/005 , B01D53/1475 , B01D53/77 , B01D2256/24 , B01D2257/504 , C07C7/11 , C10G9/206 , C10G2400/20 , Y02C10/06 , Y02P20/152 , Y02P20/51 , Y02P20/52 , Y02P30/40 , Y02P30/442 , C07C11/06 , C07C11/04
摘要： Processing schemes and arrangements for the amine treatment of high olefin content (e.g., ethylene-rich) carbon dioxide-containing streams such as for the effective separation and removal of carbon dioxide therefrom are provided. Corresponding or associated processing schemes and arrangements for the catalytic cracking of a heavy hydrocarbon feedstock and obtaining light olefins substantially free of carbon dioxide via absorption-based product recovery are also provided.
摘要翻译： 提供了用于胺处理高烯烃含量（例如富含乙烯的二氧化碳）流的方法和装置，以便有效分离和除去二氧化碳。 还提供了通过基于吸收的产物回收的重烃原料的催化裂化和获得基本上不含二氧化碳的轻质烯烃的相应或相关的处理方案和装置。
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公开(公告)号：US08383538B2
公开(公告)日：2013-02-26
申请号：US13399285
申请日：2012-02-17
申请人： Manuela Serban , Kurt M. Vanden Bussche , Alakananda Bhattacharyya , Luigi Laricchia , John P. Brady , David N. Myers
发明人： Manuela Serban , Kurt M. Vanden Bussche , Alakananda Bhattacharyya , Luigi Laricchia , John P. Brady , David N. Myers
IPC分类号： C10G21/28
CPC分类号： C10G21/06 , B01D11/0446 , B01D11/0488 , B01D11/0492 , C10G21/28 , C10G2300/1055 , C10G2300/301 , C10G2300/805
摘要： One exemplary embodiment can be an apparatus for treating a hydrocarbon stream having one or more compounds with a boiling point of about 140° to about 450° C. The apparatus can include an extraction zone and a regeneration zone. The extraction zone can include at least one settler. Each settler can have a height and a length. Typically the length is greater than the height. Also, the settler can form a boot, which can be adapted to receive a feed at one end. The regeneration zone may include a regenerator for an ionic liquid. The regenerator can include a column adapted to provide a regenerated ionic liquid to the extraction zone.
摘要翻译： 一个示例性实施方案可以是用于处理具有沸点为约140℃至约450℃的一种或多种化合物的烃流的设备。该设备可以包括提取区和再生区。 提取区可以包括至少一个沉降器。 每个定居者都可以有一个高度和一个长度。 通常长度大于高度。 此外，定居者可以形成一个引导件，它可以适应于在一端接受饲料。 再生区可以包括用于离子液体的再生器。 再生器可以包括适于向再提取区提供再生离子液体的柱。
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6.发明申请PRODUCTION OF DIESEL FUEL FROM BIORENEWABLE FEEDSTOCKS WITH SELECTIVE SEPARATION OF CONVERTED OXYGEN 有权通过选择性分离转化的氧气生产可再生能源的柴油燃料公开(公告)号：US20110245553A1
公开(公告)日：2011-10-06
申请号：US13157002
申请日：2011-06-09
申请人： Tom N. Kalnes , Terry L. Marker , John P. Brady
发明人： Tom N. Kalnes , Terry L. Marker , John P. Brady
IPC分类号： C10G3/00
CPC分类号： C10G3/45 , B01D2257/504 , C10G3/46 , C10G3/47 , C10G3/50 , C10G45/58 , C10G2300/1003 , C10G2300/1007 , C10G2300/1014 , C10G2300/1018 , C10G2300/201 , C10G2300/207 , C10G2300/4081 , C10G2400/04 , C10L1/08 , Y02E50/13 , Y02P30/20
摘要： A process has been developed for producing diesel boiling range fuel from renewable feedstocks such as fats and oils from plants and animals where the process provides for sulfur-component management. The process involves catalytically treating a renewable feedstock by hydrogenating and deoxygenating to provide a hydrocarbon fraction useful as a diesel boiling range fuel. A selective separation such as a hot high pressure hydrogen stripper may be used to remove at least the carbon oxides from the first zone effluent and provide a liquid recycle stream at pressure and temperature. A vapor stream is separated from the net process effluent and at least carbon dioxide is removed using at least one selective or flexible amine absorber. The resulting hydrogen-rich stream is recycled to the reaction zone.
摘要翻译： 已经开发了一种从可再生原料生产柴油沸点燃料的方法，例如来自植物和动物的脂肪和油，其中该方法提供硫成分管理。 该方法涉及通过氢化和脱氧催化处理可再生原料以提供可用作柴油沸程燃料的烃馏分。 选择性分离如热的高压氢气汽提器可用于从第一区流出物中至少除去碳氧化物，并在压力和温度下提供液体循环流。 蒸汽流与净处理流出物分离，并且使用至少一种选择性或柔性胺吸收剂除去至少二氧化碳。 将所得富氢流循环至反应区。
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7.发明授权Integrated warm gas desulfurization and gas shift for cleanup of gaseous streams 有权综合暖气脱硫和气体排放，用于清理气流公开(公告)号：US07935324B2
公开(公告)日：2011-05-03
申请号：US12328496
申请日：2008-12-04
IPC分类号： B01D53/48 , B01D53/62 , B01D53/02 , B01D53/86 , B01D53/96 , C01B17/16 , C01B31/20 , B01J8/00
CPC分类号： B01D53/75 , B01D53/1456 , B01D53/58 , B01D53/64 , B01D53/8618 , B01D53/864 , B01D2256/16 , B01D2257/304 , B01D2257/308 , B01D2257/406 , B01D2257/408 , B01D2257/502 , B01D2257/504 , B01D2257/602 , B01D2257/706 , B01D2259/4009 , C01B3/16 , C01B3/56 , C01B2203/0288 , C01B2203/0415 , C01B2203/045 , C01B2203/0475 , C01B2203/0485 , C01B2203/82 , C01B2203/84 , Y02C10/04 , Y02P20/152
摘要： The present invention involves a catalytic process for purifying a gas stream comprising purifying the gas stream at a temperature from about 250° to 550° C. by removing sulfur compounds and including a gas shift reaction to convert carbon monoxide to carbon dioxide to produce a partially purified gas stream. The warm gas stream purification involves COS hydrolysis and hydrogenation to H2S, the removal of H2S, and a CO gas shift to convert CO to CO2 to produce a partially purified stream. Then the carbon dioxide and other impurities are removed from the partially purified gas stream.
摘要翻译： 本发明涉及用于纯化气流的催化方法，其包括在约250℃至550℃的温度下净化气流，通过除去硫化合物并包括气体转换反应将一氧化碳转化为二氧化碳以产生部分 净化气流。 温暖的气体流净化涉及COS水解和氢化至H 2 S，除去H 2 S和CO气体转移以将CO转化为CO 2以产生部分纯化的流。 然后从部分纯化的气流中除去二氧化碳和其它杂质。
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公开(公告)号：US20090229172A1
公开(公告)日：2009-09-17
申请号：US12403024
申请日：2009-03-12
申请人： John P. Brady , Tom N. Kalnes , Terry L. Marker
发明人： John P. Brady , Tom N. Kalnes , Terry L. Marker
CPC分类号： C10G3/50 , C10G3/46 , C10G65/043 , C10G65/12 , C10G2300/1014 , C10G2300/1018 , C10G2300/1037 , C10G2300/4081 , C10G2300/80 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10G2400/28 , C10L1/026 , Y02E50/13 , Y02P30/20 , Y02T50/678
摘要： A process has been developed for producing a diesel boiling point range product and an aviation boiling point range product from renewable feedstocks such as plant and animal oils. The process involves treating a renewable feedstock by hydrogenating and deoxygenating to provide a hydrocarbon fraction which is then isomerized and selectively cracked to form the diesel boiling point range product and the aviation boiling point range product. A portion of the diesel boiling point range product, aviation boiling point range product, naphtha product, LPG, or any combination thereof can be optionally used as a rectification agent in the selective hot high pressure hydrogen stripper to decrease the amount of product carried in the stripper overhead.
摘要翻译： 已经开发了用于生产柴油沸点范围产物和来自可再生原料如植物油和动物油的航空沸点范围产物的方法。 该方法包括通过氢化和脱氧来处理可再生原料以提供烃馏分，然后异构化并选择性裂化形成柴油沸点范围产物和航空沸点范围产物。 柴油沸点范围产品，航空沸点范围产品，石脑油产品，LPG或其任何组合的一部分可以任选用作选择性热高压氢气汽提器中的精馏剂，以减少在 汽提塔头顶。
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9.发明申请Production of Diesel Fuel from Biorenewable Feedstocks with Selective Separation of Converted Oxygen 有权从生物可利用原料生产可转化氧选择性分离的柴油公开(公告)号：US20090077868A1
公开(公告)日：2009-03-26
申请号：US12193196
申请日：2008-08-18
申请人： John P. Brady , Tom N. Kalnes , Terry L. Marker
发明人： John P. Brady , Tom N. Kalnes , Terry L. Marker
IPC分类号： C10L1/18
CPC分类号： C10L1/08 , C10G2300/1003 , C10G2300/1007 , C10G2300/1014 , C10G2300/1018 , C10G2300/207 , C10G2300/4081 , C10G2400/02 , C10G2400/04 , C10G2400/28 , Y02E50/13 , Y02P30/20
摘要： A process has been developed for producing diesel boiling range fuel from renewable feedstocks such as plant and animal fats and oils, the process providing for sulfur management. The process involves catalytically treating a renewable feedstock by hydrogenating and deoxygenating to provide a hydrocarbon fraction useful as a diesel boiling range fuel. The hydrocarbon fraction is isomerized to improve cold flow properties. A selective separation such as a hot high pressure hydrogen stripper is used to remove at least the carbon oxides from the first zone effluent before entering the isomerization zone, and to provide liquid recycle to the treating zone at pressure and temperature. A vapor stream is separated from the isomerization effluent and at least carbon dioxide is removed using at least one selective or flexible amine solution absorber. The resulting hydrogen-rich stream is recycled to the deoxygenation reaction zone
摘要翻译： 已经开发了用于从可再生原料如植物和动物脂肪和油生产柴油沸点燃料的方法，该方法提供了硫的管理。 该方法涉及通过氢化和脱氧催化处理可再生原料以提供可用作柴油沸程燃料的烃馏分。 烃馏分异构化以改善冷流动性能。 在进入异构化区之前，使用诸如热高压氢气汽提器的选择性分离来从第一区流出物中至少除去碳氧化物，并在压力和温度下向处理区提供液体循环。 将蒸汽流与异构化流出物分离，并使用至少一种选择性或柔性的胺溶液吸收剂除去至少二氧化碳。 将所得富氢流循环至脱氧反应区
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10.发明授权Production of diesel fuel from biorenewable feedstocks with selective separation of converted oxygen 有权从生物可再生原料生产柴油，并选择性分离转化的氧气公开(公告)号：US08865954B2
公开(公告)日：2014-10-21
申请号：US13157002
申请日：2011-06-09
申请人： Tom N. Kalnes , Terry L. Marker , John P. Brady
发明人： Tom N. Kalnes , Terry L. Marker , John P. Brady
CPC分类号： C10G3/45 , B01D2257/504 , C10G3/46 , C10G3/47 , C10G3/50 , C10G45/58 , C10G2300/1003 , C10G2300/1007 , C10G2300/1014 , C10G2300/1018 , C10G2300/201 , C10G2300/207 , C10G2300/4081 , C10G2400/04 , C10L1/08 , Y02E50/13 , Y02P30/20
摘要： A process has been developed for producing diesel boiling range fuel from renewable feedstocks such as fats and oils from plants and animals where the process provides for sulfur-component management. The process involves catalytically treating a renewable feedstock by hydrogenating and deoxygenating to provide a hydrocarbon fraction useful as a diesel boiling range fuel. A selective separation such as a hot high pressure hydrogen stripper may be used to remove at least the carbon oxides from the first zone effluent and provide a liquid recycle stream at pressure and temperature. A vapor stream is separated from the net process effluent and at least carbon dioxide is removed using at least one selective or flexible amine absorber. The resulting hydrogen-rich stream is recycled to the reaction zone.
摘要翻译： 已经开发了一种从可再生原料生产柴油沸点燃料的方法，例如来自植物和动物的脂肪和油，其中该方法提供硫成分管理。 该方法涉及通过氢化和脱氧催化处理可再生原料以提供可用作柴油沸程燃料的烃馏分。 选择性分离如热的高压氢气汽提器可用于从第一区流出物中至少除去碳氧化物，并在压力和温度下提供液体循环流。 蒸汽流与净处理流出物分离，并且使用至少一种选择性或柔性胺吸收剂除去至少二氧化碳。 将所得富氢流循环至反应区。
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